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N A N O E X P R E S S

A Kind of Nanofluid Consisting of Surface-Functionalized

Nanoparticles

Xuefei Yang•Zhen-hua Liu

Received: 18 March 2010 / Accepted: 10 May 2010 / Published online: 25 May 2010

ÓThe Author(s) 2010. This article is published with open access at Springerlink.com

Abstract A method of surface functionalization of silica nanoparticles was used to prepare a kind of stable nano-fluid. The functionalization was achieved by grafting silanes directly to the surface of silica nanoparticles in silica solutions (both a commercial solution and a self-made silica solution were used). The functionalized nano-particles were used to make nanofluids, in which well-dispersed nanoparticles can keep good stability. One of the unique characteristics of the nanofluids is that no deposi-tion layer forms on the heated surface after a pool boiling process. The nanofluids have applicable prospect in ther-mal engineering fields with the phase-change heat transfer. Keywords NanofluidSurface functionalization NanoparticleHeat transferPhase change

Introduction

Nanofluids, proposed firstly by Choi [1], are dispersions of nanoparticles (metals, oxides, nitrides and carbon materials etc.) in base fluids (water, ethylene glycol and engine oil etc.). They have wide ranges of applications, e.g., to enhance heat transfer [1–11], as magnetic nanofluids [12] and other special applications [13–18]. However, long-term stability of nanofluids is a major concern for the engi-neering applications [3, 10,17]. Nanoparticles tend natu-rally to aggregate and sediment in the base fluid. Also, stable solution with large volume concentration is not easy

to obtain. Therefore, technique breakthroughs are needed to produce well-dispersed and long-term stable nanofluids. Use of functionalized nanoparticles is a promising approach to achieve long-term stability of nanofluid. Functionalization of silica nanoparticles has been reported earlier in literature [19–24]. The current authors have reported earlier on effects of nanoparticles in nanofluid on thermal performance in water-CuO system [14]. The present work reports on the synthesis of functionalized silica (SiO2) nanoparticles by grafting silanes directly to the surface of silica nanoparticles in original nanoparticle solutions. Nanofluids can then be prepared by just adding water into it.

Experimental

Two kinds of original silica nanoparticle solutions were used to make functionalized nanoparticles. One was a commercial nanoparticle solution, ludox TM-40, purchased from Aldrich company in USA. The ludox TM-40 (with the silica nanoparticle mass concentration of 40% in water, the average diameter of nanoparticles of about 30 nm) contains NaOH, surfactants and so on to stabilize the silica nano-particles in the water solution. The other was a self-made nanoparticle solution prepared by the two-step method. Silica nanoparticle powders were firstly dispersed into deionized water, and the suspension was then oscillated in an ultrasonic bath for 12 h. Silica nanoparticle powders with an average diameter of about 30 nm were commercial products of gas condensation.

Two silanes of 2-[methoxy (polyethyleneoxy) propyl] trimethoxysilane (MPPTS) and (3-glycidoxylproyl) trime-thyoxysilane (GPS) were received from Gelest company in USA and used without further purification.

X. YangZ. Liu (&)

School of Mechanical Engineering, Shanghai Jiaotong University, 800 Dongchuan Road, 200240 Shanghai, People’s Republic of China

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The schematic of the functionalization is shown in Fig.1. The synthesis methods using two silanes are described as follows:

(1) MPPTS-functionalized nanoparticles

MPPTS-functionalized nanoparticles were synthesized simply by grafting directly a certain amount of MPPTS to silica nanoparticles in silica solutions. As an example, 25 g of Ludox TM-40 was diluted with 50 g deionized water. To the silica suspension, 1.45 g of MPPTS was added drop-wise under vigorous stirring at room temperature. Gener-ally, the mass ratio (defined as the ratio of the mass of the silane to that of the silica nanoparticles in silica solutions) ranges from 0.1 to 1.0. The entire mixture was heated to 70°C and stirred and oscillated vigorously for 48 h at that temperature. The obtained solution was then dialyzed in the snakeskin dialysis tubing (3.5 k MWCO, purchased from Pierce) with deionized water as the dialyzate for 48 h and thereafter freeze-dried to give white fine nanoparticle powders.

(2) GPS-functionalized nanoparticles.

GPS-functionalized nanoparticles were synthesized in a similar manner. Generally, the mass ratio ranges from 0.1 to 1.0. As an example, 1.35 g of GPS was diluted with 10 g of deionized water, and the pH value of the solution was adjusted to 2 with dilute HCl. After vigorous stirring for 4 h at room temperature, its pH value was adjusted to 10 with dilute NaOH. Meanwhile, 25 g of Ludox TM-40 was diluted with 40 g of deionized water. The obtained GPS solution was then added dropwise to the silica suspension under vigorous stirring and oscillation and kept at 70°C for 48 h in an ultrasonic bath. The obtained solution was then purified by dialysis and freeze-dried in the same manner shown earlier.

Obtained fine nanoparticle powders were the function-alized nanoparticles.

Results and Discussion

Properties of the Functionalized Nanoparticles

To investigate the reaction degree of the silica and the silane, TGA instrument (TA Q5000) was used to analyze how many silanes are grafted on the silica nanoparticles. The fine powders of functionalized nanoparticles were burnt at 700°C in a TGA instrument, and the organic

components on the surfaces of the functionalized nano-particles were burnt away. The TGA instrument can record the mass loss of the functionalized nanoparticles during the whole process. Table1 shows the mass loss percentage caused by the organic components for functionalized nanoparticles at different mass ratio. The mass ratio is the ratio of the mass of the reacting silane to that of the reacting silica. The mass loss is the mass loss percentage of the functionalized silica before and after the TGA process. Results show that the mass loss increases with the increase in the reacting mass ratio. More silanes can be grafted on the silica nanoparticles at larger mass ratios. At the same mass ratio, the nanoparticles functionalized with MPPTS have a larger mass loss compared to those with GPS.

After the functionalization process, nanofluids were prepared by the two-step method using functionalized nanoparticles and deionized water. Functionalized nano-particles were dispersed into deionized water, and the solution was thereafter vigorously stirred and oscillated in an ultrasonic bath for 12 h at room temperature (the solu-tion can also be standing for 12 h with the environmental temperature of 50°C). Then, well-dispersed nanofluid can be prepared without any surfactant used. Functionalized nanoparticles can still keep dispersing well after the nanofluid has been standing for 6 months and no sedi-mentation was observed. The dispersing state of function-alized nanoparticles after 6 months is still under investigation and will be reported later.

Figure2a and b are the transmisson electron microscope (TEM) pictures of nanofluids consisting of nanoparticles before and after the functionalizing process (prepared with ludox TM-40 and MPPTS, the mass ratio is 0.123), respectively. Figure2c and d are the TEM pictures of nanofluids consisting of nanoparticles before and after the functionalizing process (prepared with self-made nano-particle solution and GPS, the mass ratio is 0.115), respectively. The nanoparticle mass concentration is 1.0%. As is shown, functionalized nanoparticles have no aggre-gation and can disperse well. In the present study, the mass concentration of the functionalized nanofluid (nanofluids consisting of functionalized nanoparticles) prepared with commercial silica solution can go beyond 50%, and the other functionalized nanofluid prepared with self-made silica solution can reach maximally 10% under the condi-tion that no aggregacondi-tion occurs.

Dynamic light scattering (DLS) measurement of func-tionalized nanoparticles was taken using a Malvern Zeta-sizer Nano particle characterization system. Diameter distribution of functionalized nanoparticles (prepared with self-made and GPS, the mass ratio is 0.115) is indicated in Fig.3. The average diameter of the functionalized nano-particles is about 30 nm, which is in consistent with the result shown in Fig.2.

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Surface State of Heated Surface After Pool Boiling Process Using Functionalized Nanoparticles

An applicable prospect of functionalized nanofluids is in the phase-change heat transfer. Up to now, almost all phase-change heat transfer studies of conventional nanofl-uids (consisting of nanoparticles without functionalization)

reported that nanoparticles fouled on the heated surface after the boiling process. A thin porous layer formed on the heated surface and affected strongly the boiling characteristics.

[image:3.595.51.544.73.162.2]

In order to investigate the heat transfer characteristics of functionalized nanofluids in the phase-change heat transfer, a pool boiling experiment using both the conventional

Table 1 Mass loss of functionalized nanoparticles after the TGA process

MPPTS GPS

Mass ratio Mass loss (%) Mass ratio Mass loss (%)

Silica in ludox TM-40 0.491 14.16 0.460 13.83

0.246 11.12 0.230 7.71

0.123 7.36 0.115 5.85

Silica in self-made nanoparticle solution 0.123 7.18 0.115 5.52

Mass ratio represents the mass ratio of the reacting silane and silica; mass loss represents the mass loss percentage caused by the organic components after the functionalized nanoparticles are burnt by the TGA instrument

Fig. 2 TEM pictures of nanofluids consisting of nanoparticles before and after the functionalizing processananoparticles in ludox TM-40

bfunctionalized nanoparticles prepared with ludox TM-40 and MPPTS

[image:3.595.114.480.202.574.2]
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nanofluid and the functionalized nanofluid was carried out on a smooth copper surface positioned horizontally. The experimental system and the procedure were the same as author’s previous study [11]. The copper surface had an average roughness of 194 nm. The experiment was carried out at atmospheric pressure with the fluid temperature of about 100°C. The copper surface was kept heating for 3 h with the heat flux of about 500 kW/m2. Figure4a shows the SEM picture of the heated surface before the boiling experiment. Figure4b and c show the SEM pictures of the heated surface after the boiling experiment using both the functionalized nanofluid (consisting of functionalized nanoparticles prepared with self-made nanoparticle solu-tion and GPS, the mass ratio is 0.115) and the original self-made nanofluid. The mass concentration of nanoparticles in the two nanofluids is 1.0 wt%. It was found that no porous fouling layer formed on the heated surface after boiling process using the functionalized nanofluid. Only scattered functionalized nanoparticles attach on the heated surface. The nanoparticles can be easily flushed away by water. However, a fouling layer of nanoparticles forms on the heated surface after the boiling experiment using the ori-ginal self-made silica solution. The fouling layer cannot be flushed away by water. The development of this layer is a direct consequence of boiling of nanofluids. The evapora-tion of nanofluids with subsequent settlement of unfunc-tionalized nanoparticles initially contained in it could be the reason for the formation of this layer. Nanoparticles without functionalization cannot easily resolve in the base fluid. It is not the case, however, for functionalized nano-particles since their improved solubility.

Since no fouling layer exists after the boiling process, the functionalized nanofluid can be applicable in heat pipes that utilize the phase-change heat transfer of working fluids to dissipate heat. This is quite helpful for the long-term stable running of heat pipes since the heated surfaces keep the same and the nanofluid keep dispersing well. Further experiment is undergoing for better understanding the application of functionalized nanofluids in heat pipes. In addition, the well-dispersed and stable functionalized nanofluid can be applicable to microchannels in electronic devices and compact cooling modules to dissipate heat more effectively. It is also useful for enhancing the mass transfer, such as the oxygen absorption in chemical and biochemical industry, ammonia absorption in the refriger-ation technique.

Mechanism of the Functionalization

The Derjaguin–Landau–Verwey–Overbeek (DLVO) theory of colloid stability is commonly used to describe the par-ticle–substrate interfacial interactions in the base fluid [25]. In this theory, both an attractive force and a repulsive force existing between particles account for the stability of par-ticles in the base fluid. The attractive force, also called the van der Waals force, includes attractions between atoms, molecules and surfaces. It grows with the length of the nonpolar part of the substance. The van der Waals force is relatively weak compared to normal chemical bond. The repulsive force arises from the overlap of electrical double layers that appear on the surfaces of particles when they are placed into the base fluid. The overlap of their double layers interrupts their own electrostatic stability and the electrostatic repulsion causes the repulsive force, when two particles get too close together. Particles in the base fluid can keep stable if the repulsive force is stronger than the attractive force. Otherwise, particles will aggregate. Seri-ous aggregation of particles may lead to the sedimentation of particles.

Another theory named as the steric stabilization effect is also a key explanation for the stability of particles in the

Fig. 4 SEM pictures of the heated surface during the boiling experimentabefore the boiling experimentbusing the functionalized nanofluid

cusing the conventional nanofluid

[image:4.595.52.289.58.141.2] [image:4.595.90.511.576.686.2]
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base fluid [25]. The steric stabilization effect arises from the fact that polymers gathering on the surface of nano-particles occupy a certain amount of space. If nanonano-particles are brought too close together, the space is compressed. An associated repulsive force helps separate nanoparticles from each other and restrains the aggregation of nanoparticles.

Adding ions to the nanofluid according to the DLVO theory can enhance the electrostatic repulsion of nanopar-ticles. Adding surfactants to the nanofluid is helpful for the steric stabilization effect. These are ways how ludox TM-40 is treated to help the silica nanoparticles stabilize in the water solution. In ludox TM-40, anions (like OH-) are used to stabilize silica nanoparticles. But nanoparticles may be applied in acidic or neutral conditions. Also, the steric effect by surfactants may be broken down when the nanofluid is heated or the Brownian motion of nanoparti-cles is extremely strong. A better way, as is indicated in this paper, is to graft polymers onto the surface of nano-particles. The grafting is achieved with the covalent bonding, which is quite stable and not easy to be broken down. The chosen silanes can react with the silica nano-particle. The grafting silanes on nanoparticles have the steric stabilization effect to stabilize nanoparticles. The covalent bonding ‘‘Si–O–Si’’ is stable chemical bonding to facilitate the application of functionalized nanoparticles regardless of the working conditions, like the heated case. Besides, to achieve a better and larger solubility of nanoparticles in water, silanes containing polar structures are chosen. Due to the solubility rule of similarity, polar substances are soluble with each other. The polar structure grafted on the surface of the silica nanoparticles increases the solubility of functionalized nanoparticles in water (which is also a polar substance). The mentioned MPPTS and GPS are two of those.

The nanofluids with functionalized nanoparticles gain the merits of good dispersing, stable bonding, no surfactants needed and large solubility. Similar methods may be used to other nanoparticles for heat transfer applications. The functionalized nanofluid made by commercial product of ludox TM-40 can prepare the nanofluid with a higher nanoparticle mass concentration. However, using the func-tionalized nanofluid prepared by the cheap self-made silica solution is a more economic way for industrial application due to its cheap price and large producing capacity.

Conclusion

A method of surface functionalization of silica nanoparti-cles to prepare a kind of functionalized nanofluid was

presented. The functionalization was achieved by grafting silanes directly to the surface of silica nanoparticles. Then, the obtained functionalized nanoparticles were used to prepare the nanofluid. The nanofluid with functionalized nanoparticles can keep long-term stability and very good dispersing. Functionalized nanoparticles can still keep dispersing well after the nanofluid has been standing for 6 months and no sedimentation is found. One unique characteristic of the functionalized nanofluids is that no porous sediment layer forms on the heated surface after boiling process.

Open Access This article is distributed under the terms of the Creative Commons Attribution Noncommercial License which per-mits any noncommercial use, distribution, and reproduction in any medium, provided the original author(s) and source are credited.

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Figure

Table 1 Mass loss of functionalized nanoparticles after the TGA process
Fig. 3 Diameter distribution of functionalized nanoparticles

References

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